US3810820A - Urate oxidase and process for the production thereof - Google Patents
Urate oxidase and process for the production thereof Download PDFInfo
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- US3810820A US3810820A US00180220A US18022071A US3810820A US 3810820 A US3810820 A US 3810820A US 00180220 A US00180220 A US 00180220A US 18022071 A US18022071 A US 18022071A US 3810820 A US3810820 A US 3810820A
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/0004—Oxidoreductases (1.)
- C12N9/0012—Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7)
- C12N9/0044—Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7) acting on other nitrogen compounds as donors (1.7)
- C12N9/0046—Oxidoreductases (1.) acting on nitrogen containing compounds as donors (1.4, 1.5, 1.6, 1.7) acting on other nitrogen compounds as donors (1.7) with oxygen as acceptor (1.7.3)
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- Y10S435/814—Enzyme separation or purification
- Y10S435/815—Enzyme separation or purification by sorption
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- Y10S435/939—Rhizopus
Definitions
- the invention relates to a new enzyme or urate oxidase which is very active in promoting oxidation of uric acid to allantoin.
- the urate oxidase is produced by fermentation under aerobic conditions of nutrient media containing sources of assimilable carbon, assimilable nitrogen and uric acid which have been seeded with suitable cultures of bacteria, fungi or yeasts. Isolation and purification of the urate oxidase is described.
- This invention relates to a novel urate oxidase having a high activity (currently known by the name uricase), as well as to a process for the manufacture thereof.
- uric acid is one of the principal products of the catabolism of purine bases and of the products which they contain, such as nucleic acids. It is also known that if catabolism does not take place or elimination of uric acid does not occur, this product can accumulate inthe blood or the tissues and can be the cause of many disorders, especially of gout, certain forms of rheumatism, certain calculi in the region of the urinary system and various tissue changes, especially in the cardio-vascular system.
- the uricase of the present invention is obtained from active strains of micro-organisms which are either bacteria, especially those of the genus Bacillus, or fungi especially those which belong to the genera Mucor, Rhizopus, Absidia, Fusarium, Alternaria, Penicilliurn, Aspergillus, Cephalosporium, Stemphylium and Macrosporum, or yeasts, especially of the genus Geotrichum. These genera belong to the orders of eubacteriales, actinomycetales, mucorales, moniliales, spheriales and endomycetales.
- the uricase may also be obtained using bacteria of the genera Pseudomonas, Clostridium, Micrococcus and Bacterium, fungi of the genus Neurospora and yeasts of the genera Saccharomyces and Torula (Candida).
- the invention comprises more particularly the production of the uricase using bacteria and fungi belonging to the species Streptomyces cellulosae and Strept. sulfureus, Bacillus megatherium, B. subtilis and B. cerus, Aspergillus flavus, Asp. oryzae, Asp. tamarii, Asp. terricola, Asp. luchuensis, Asp. niger, Asp. sydowi, Asp. nidulans, Asp. wemii,,Asp. fonsecaeus, Asp. clavatus, Asp. ustus, Asp. terreus and Asp. ochraceus, Penicillium frequentans, Pen.
- Pen. griseum granulatum
- Pen. canescens Pen. spinulosum
- Pen. thomii Plen. waksmani
- Pen. raistrickii Pen. expansum
- Pen. purpurescens Pen. funiculosum, Pen.
- Suitable microorganisms are given below. In this list each name is followed by the number assigned by the applicants to the strain in their collection and in brackets by the registered number of the strain deposited in the American Type Culture Collection (A.T.C.C.).
- coeruleum Saccardo 727 (20088), Fus. oxysporum Schelechtendahl 735(20089), Stemphylium macrosporoideum Saccardo 700(20090), Macrasporium apiospermum 653(20091), Fusalrium orthoceras Appel & Wollenweber 729(20092), Absidia Glauca+ (Hagem) 1801 (20093), Mucor mucedo Brefeld 1202(20094), Mucor hiemalis Wehmer 1205(20095), Mucor racemosus Fresnius 1209 (20096), Rhizopus arrhizus Fisher 1212(20097), Basidiomycete sp. 1500 (20098).
- the invention also includes a process for producing and purifying the urate oxidase thus making it possible to obtain the product in a very active form.
- This activity expressed in uricase units, in accordance with a definition which will be given hereafter, is generally between 10 and 3 500 units per milligram. The method of measuring the activity is described subsequently.
- a process for producing a urate oxidase which promotes the oxidation of uric acid to allantoin which comprises cultivating an active strain of a bacterium, a fungus or a yeast in or upon an aqueous nutrient medium comprising an assimilable source of carbon, a source of assimilable nitrogen, and uric acid under conditions of aerobic fermentation, separating the culture from the aqueous medium and isolating said urate oxidate from the culture and/or from the resulting aqueous medium.
- the process of the invention involves cultivating the urate oxidase producing micro-organism, either by using a submerged pre-culture, sparsely or not sporulated, entirely in a liquid medium which is suitably agitated and aerated, making it possible to produce considerable amounts of the microorganism, preferably at tempera tures between 20 and 35 C. and during 4 to 12 days of cultivation, or by cultivation entirely upon a solid medium making it possible to obtain spores at temperatures between 20 and 35 'C. during 6 to 15 days of cultivation.
- the thus prepared inoculum is used to seed a nutrient medium containing urate ions and in effecting fermentation at a temperature which is preferably between and 35 C.
- the microbiological mass is separated from the liquid phase, preferably when maximum production has been attained, and the urate oxidase is extracted from the microbiological mass and/or from the liquid phase.
- the crude urate oxidase thus obtained is then purified.
- inoculum pre-cultivation in depth may be carried out in a Czapeck-Dox or in a Sabouraud medium. If it is desired to use a solid medium, the culture may be effected upon malted rice.
- Extraction of the endocellular urate oxidase from the micro-biological mass may be effected by solidifying this mass, pulverizing it and submitting the pulverized material to a solid-liquid extraction procedure.
- a preferred strain of mycelium which is highly active is one obtained from an enriched culture of the genus Aspergillus and of the species flavus.
- the process is applicable to other micro-organisms which produce endocellular urate oxidase in particular but not exclusively to those micro-organisms which have been set out above.
- An analogous process may be used for those microorganisms which produce exocellular urate oxidase, by treating the filtrates of the culture medium in the same manner as the cellular extracts of micro-organisms which produce the endocellular urate oxidases.
- the culture media should contain all the organic and inorganic constituents which are necessary for satisfactory development of the micro-organism and for the production of uricase in high yield. They should contain: (a) a source of assimilable carbon, in particular but not exclusively simple sugars such as glucose or saccharose, alone or in admixture, in concentrations between 1 and 10% by weight (with respect to the total weight of the culture medium); (b) a source of assimilable nitrogen which is usually supplied in the form of inorganic nitrogen, such as ammonium chloride or sulphate, or an alkali nitrate, in concentrations between 1 and 10% by weight; and (c) inorganic elements such as phosphorus, magnesium, potassium, sodium, calcium and iron, in concentrations gen erally between 0.0001 and 0.5% by weight, as well as uric acid, in an amount between 0.01 and 0.2% 'by weight as an inductor.
- a source of assimilable carbon in particular but not exclusively simple sugars such as glucose or
- oligodynamic substances such as amino acids, vitamins and growth factors, nucleotides and inorganic trace elements such as manganese, molybdenum, copper, cobalt and zinc.
- these substances may be supplied, for example, by yeast extracts, malt extracts or by the hydrolysis products of animal and/or vegetable proteins or by inorganic salts. These may be used in concentrations between 0.0001 and 0.5% by weight.
- the various constituents can be added either partially or entirely when preparing the culture medium, prior to seeding, or during the course of the fermentation and, in the case of certain elements, on account of their special importance, during the synthesis of the enzyme.
- the constituents are essentially, but not exclusively, nitrogen and phosphorus-containing constituents and uric acid.
- Cultivation is generally effected in depth employing agitation and aeration. Agitation may be by stirring which may vary, depending upon the installation used, between 10 and 200 rpm. Aeration is preferably effected at a rate between 0.05 and 0.5 litres of medium per minute. Sufficient agitation can be achieved by bubbling through air. It should be noted however that agitation and aeration conditions which lead to too rapid and too intensive development of the mycelium may be prejudicial to optimum production of the enzyme.
- DURATION OF THE CULTIVATION Cultivation is continued, preferably, until optimum enzyme activity is attained, this being determined by the analytical method which will be subsequently described. It is recommended that the fermentation be carried out to a substantially constant value of optimum enzyme ac tivity, rather than to a value, which is possibly greater but is transitory.
- the culture generally attains maximum activity after from 15 to 60 hours culture; this time varies with the nature of the culture medium, the strain of inoculum employed and the conditions of cultivation.
- the culture medium is filtered in order to separate the mycelium; the latter is washed with water and thereafter pulverized for the purpose of extracting the uricase.
- pulverisation it is possible to freeze the mycelium at low temperatures by means of carbon dioxide ice or carbon dioxide snow or by any other process which makes it possibile to freeze the mycelial mass rapidly and completely.
- freezing is carried out at temperatures between -15 and 30 C.
- the mycelium is thereafter pulverized in an apparatus which enables complete separation of the mycelial constituents, without modifying the enzyme.
- the pulverized product is extracted in water containing a buffer agent or in aqueous ammonia, brought to a pH which is preferably between 7 and 10, preferably 8.5, for the purpose of extracting the enzyme. This operation is carried out at a temperature below 30 C. by using a suitable extraction process. Moreover, in order to render the extract more stable a complexing agent may be added in a concentration of the order of 0.001 M, for example ethylenediamine tetraacetic acid, generally in the form of the sodium salt. The suspension is thereafter filtered and dried.
- the mycelial extract thus obtained contains the uricase together with numerous proteins and other substances, in solution or in a colloidal state; they may have to be removed by desiccation or by means of salts with which they form complexes.
- Suitable salts include calcium salts, such as calcium chloride and lead salts such as lead acetate, which make it possible to eliminate a great number of impurities in the form of insoluble compounds.
- an antibiotic such as chloramphenicol, or an antiseptic, for example sodium azide, in amounts which may be between and 500 eg/ml, preferably 100 neg/ml.
- the uricase being soluble in water but insoluble in organic solvents and in concentrated aqueous solutions of inorganic salts such as ammonium sulphate, can be recovered easily, either by precipitation with the aid of an organic liquid which is miscible with water, for example ethanol, methanol or isopropanol or more preferably acetone, used in the proportion of 0.5 to 3 volumes per volume of extract, or by salting out with a watersoluble salt especially with a saturated solution of ammonium sulphate at room temperature, also used in a proportion of 0.5 to 3 volumes per volume of extract.
- an organic liquid which is miscible with water for example ethanol, methanol or isopropanol or more preferably acetone
- the mycelial extract may first be concentrated, by carrying out the operation under reduced pressure at a temperature below 40 C.
- the precipitate thus obtained is separated, for example by centrifuging.
- the organic liquid which it contains is removed rapidly under reduced pressure, without apply-. ing heat.
- the precipitate can then be dissolved in water for the purpose of lyophilization, after filtration or centrifuging, which results in the production of a semi-purified product.
- filtration using membranes of a filter candle is carried out prior to lyophilization.
- the salts may be removed either by dialysis or by rapid filtration using a suitable molecular sieve, for example, a dextran gel or a polyacrylamide gel.
- the substances which can be used for this purpose include columns of cellulose ion exchange materials, dextrans and polyacrylamides. Elution may be effected by means of liquids in which there is a continuous or discontinuous change in the pH or in the molarity thereof.
- the uricase is obtained in the form of an amorphous, colorless or slightly yellow powder which is soluble in water and the conventional buffer solutions, the solubility being greater in alkaline solution than in an acid solution. It is insoluble in the usual organic solvents such as ethanol, methanol, acetone, diethyl ether and chloroform.
- the pH of solutions having optimum activity is 8.5 and the temperature at which the uricase exhibits optimum activity is 30, the activity is, however still quite high at 37 C.
- the activity of the uricase is partially inhibited by the following cations: Zn++, Cd++, Mn++, Fe+++, Co++, Ni++, Al,+++ at concentrations of 10* and 10- M, and by Hg.++ at a concentration of 10- M.
- Cu++ is a weak inhibitor (30% inhibition at 10" M). Calcium, sodium, potassium, magnesium and ammonium ions either do not or only slightly inhibit activity up to concentrations of 10" M.
- borate, carbonate, acetate, citrate, nitrate, chloride and phosphate have no efifect on the uricase at concentrations of l0 to 10- M; however the nitrate and chloride anions can become partial in hibitors at concentrations of the order of l0- M.
- the uricase has no eflect upon cafieine, theobromine, theophylline, xanthine, S-chloroxanthine of 2,8-dithio-6- hydroxypurine, that is to say, upon the principal biological products the chemical structure of which is closely similar to that of uric acid. Consequently this enzyme can be regarded as extremely specific.
- Iso-electric weight Our urate oxidase was found to have an iso-electric weight of 6.21:0.1 (6.8 for hemoglobin as a control).
- Aminoacid content The following table shows the nature and percentage (reckoned on urate oxidase dry weight) of the aminoacids in our urate oxidase.
- EXAMPLE 1 Strain Aspergillis flavus oryzae No. 624 (A.T.C.C. No. 20047).
- Inoculum Sporulated culture, grown on rice for 9 days at 28 C. in two Roux bottles each of 1 litre capacity and then taken up in two litres of physiological salt solution containing 6 g. of sodium chloride per litre.
- the culture medium was sterilized for 30 minutes at 120 C. Seeding after cooling with the inoculum described above.
- Cultivation during cultivation the temperature of the culture medium is maintained at 28 i 1 C., the culture medium is aerated by means of sterile air blown in to the bottom of the container at a rate of 0.3 litres per litre of culture medium per minute. After 24 hours of cultivation under the indicated conditions 20 kg. of mycelium having a content of 150 p../g. of uricase is obtained. The mycelium is Washed with 40 litres of sterile distilled water and then cooled rapidly to 20 C.
- the mycelium is frozen at -20 C., pulverized and then taken up in 40 litres of aqueous ammonia having a pH 9; after concentrating the solution to one-quarter of its original volume under reduced pressure and precipitation by addition of two volumes of acetone, 380 g. of a crude product containing 7000 ;t./g. of uricase is obtained. This product is taken up in 3.8 litres of a 0.002 M aqueous sodium carbonate solution. After centrifuging the solution is treated with an equal volume of a saturated aqueous solution of ammonium sulphate.
- the precipitate thus obtained is separated by centrifuging, then taken up in an aqueous solution of 0.002 M sodium carbonate; the insoluble remainder is eliminated by centrifuging.
- the supernatant solution is then freed from inorganic constituents using a column of a dextran gel buffered With 0.002 M sodium carbonate, and the active eluates are sterilized by passing them over a Millipore GS membrane and are then lyophilized. 57 g. of a product containing 49,000 ,u./g. of uricase are thus obtained.
- Inoculum This is prepared by seeding 2 litres of a Saboraud liquid medium with an agar culture on a Czapeck-Dox culture medium. After 40 hours cultivation this culture is used for inoculating 100 litres of a fermentation liquid containing the same culture medium as in Example 1. At the end of 30 hours cultivation at 28 C. this second inoculum is used for seeding the actual fermentation medium.
- Cultivation During cultivation the temperature of the culture medium is maintained at il C. and the culture medium is agitated by means of a propeller revolving at 150 r.p.in. The culture medium is aerated by means of sterile air at the rate of 0.2 liters/ liter of culture medium per minute. After 31 hours of cultivation there is added to the culture medium 2 kg. of sodium nitrate, 0.5 kg. of yeast autolysate and 0.5 kg. of uric acid, all of which have been previously sterilized. After 43 hours of cultivation kg. of mycelium containing 140 a/ g. of uricase is obtained. The mycelium is washed with sterile distilled water and then rapidly cooled to 20 C.
- the frozen mycelium is pulverized and then extracted by means of liters of aqueous ammonia having pH 9. After filtration the pH of the extract is readjusted to 9 and the volume of this extract reduced to 40- liters by concentration under reduced pressure.
- the concentrated product is purified by treatment with an aqueous solution of basic lead acetate containing 10% by weight of lead. After centrifuging the supernatant liquid which contains the uricase is admixed with 48 liters of a saturated aqueous solution of ammonium sulphate. The precipitated obtained is separated by centrifuging, taken up in 2.5 liters of a 0.002 M aqueous sodium carbonate solution and then passed through a column of a dextran gel. The active eluates are lyophilized and there is thus obtained 54 g. of a product containing 91,000 p../g. of uricase.
- EXAMPLE 3 The process described in Example 2 is repeated and there is obtained 58 g. of a product containing 87,000 ../g. of uricase. This product is dissolved in a 0.01 M ammonium carbonate solution and the solution, buffered by a 0.01 M aqueous solution of ammonium carbonate at pH 9 is passed over a column of diethylaminoethyl cellulose. The column is subsequently washed with a 0.05 M ammonium carbonate solution. The uricase is eluted from the column by increasing the molarity of the buffer solu tion during the course of the elution. There is obtained in liquid form the equivalent of 4.7 g. of a product contain 340,000 ,LL./g.
- Example 3 and 4' the activity is expressed specifical- 1y by reference to the total activity to the quantity of proteins contained in solution, determined by the microbiuret reaction, whereas in Examples 1 and 2 it is expressed with reference to the weight of the dry product.
- the uricase of this invention renders possible the rapid, specific and intensive elimination of uric acid and of urates present in the animal organism by conversion into Water-soluble allantoin. It can be used, in particular, as a laboratory product in research and analytical studies of uric acid.
- the activity is measured by determining the quantity of uricase required, under conditions hereafter described, to oxidize one half of the uric acid present in the reaction medium. The determination is based upon the fact that the optical density of a solution of uric acid falls after incubation with the enzyme preparation. Uric acid in acid solution has a maximum absorption in ultraviolet light at 285 millimicrons. The optical density under the conditions of the determination is proportional to the concentration of the uric acid and this fact makes it possible to measure the uric acid utilized and, consequently, to determine the activity of the enzyme.
- the unit of uricase activity is the quantity of enzyme which brings about the destruction of one half of the quantity of the substrate, that is of the uric acid introduced initially under the conditions of the determination.
- the culture tubes are placed upon a water bath and after a pre-incubation period of 5 minutes 1 ml. of the uric acid solution containing cg/ml. is introduced into the culture tubes 2 and 4.
- the culture tubes are then left to incubate for 10 minutes at 30 C. and the reaction is stopped by adding 0.2 M hydrochloric acid.
- Culture tubes 2 and 4 are respectively compared with tubes 1 and 3, which are used as controls, by means of an ultra violet spectrophotometer using a wavelength of 285 11111..
- Tubes 1 and 2 can be used as controls for a series of determinations of optical density. Tubes 3 and 4 are used for the actual determinations.
- Concentration of the standard solution utilized is 10 ag./ml.:0.5 ,u./ml.
- the uricase can be lyophilized in a sterile medium under conventional conditions using an aqueous solution which has been sterilized by use of a sterilizing filter such as a Millipore filter.
- the uricase has been administered to dogs. However, as the dog does not have any uric acid in its blood, an investigation of the uricase activity in the plasma was carried out by injecting the animals with the uricase. It was found that the enzyme persists in the blood for more than 24 hours, irrespective of whether it is administered intravenously, intramuscularly or subcutaneously.
- FIG. 6 of the drawings represents the action of the uricase (110 units/kg; intravenous) on the uricemia in dogs excluding the liver circulation; the uricemia, expressed in ,ucg./ml., is shown as ordinates and the time, expressed in minutes, is shown as abscissae.
- the uricase does not have any pronounced effect in dogs upon blood pressure, cardiac frequency, cardiac electrogenesis, tensional responses to various chemical mediators or upon the respiratory movements. It has no eifect in dogs on water or inorganic diuresis.
- the uricase being a protein by nature behaves as an antigen. In the course of the various tests carried out in studying the antigenic effect of this product, it did not exhibit any allergic properties but only immunizing properties.
- a rabbit which has been hyperimmunized with uricase to which there is added the adjuvant of Freund reacts by forming antibodies which. are easily detected by the method of Ouchterlony (1948, Acta. Path. Microb. Scandinav., volume 26, (1949), p. 507).
- the uricase has no acute toxicity. A dose of 10,000 units/kg. injected intravenously into mice causes no pathological symptoms.
- Toxicity tests have been carried out upon dogs using dosages of 200 and 1000 units per animal per day.
- the uricase has been administered intravenously for four months without producing any abnormal phenomenon or noticeable istological modifications in the animals.
- Table No. 1(B) sets out the results obtained. Twentyfour hours after treatment the extensive diminution of the uricemia observed in Test N0. 1 is also found to occur here. As a corollary the urinary allantoin increases very markedly.
- Uricernia Uricemia Dosage Urinary (neg. uric Urinary eg. uric Days of (units Diuresis allantoin acid/ml. Diuresis allantoin acid/ml. treatment r.v.) (ml/24 h.) (mg/24 h.) plasma) (1111/24 h.) (mg/24 h.) plasma)
- the uricase of the invention can be used in human therapeutics in the treatment of hyper-uricemia and, more generally, for resolving the pathological problems which occur when an excess of uric acid or of salts thereof are present.
- the uricase can be administered parenterally, notably by the intravenous, subcutaneous or intramuscular routes, or by oral or endorectal administration.
- compositions for intravenous administration are that of an aqueous solution which contains, at the time of application, 1000 units of lyophilized and sterilized uricase and 5 ml. of a sterilized solvent having the following formula:
- the lyophilization of the uricase was carried out in a sterile medium under the usual conditions, using an aqueous solution which had been sterilized on a sterilizing filter such as the Millipore filters.
- aqueous solutions ready for use, of a highly purified uricase containing 200 to 500 m n/mg, by storing the solutions at a sufficiently low temperature, the solutions being prepared from the highly purified uricase and from an aqueous solution of ammonium carbonate having a concentration of 0.1 M ammonium ions, this solution having been brought to pH 8 by means of carbon dioxide.
- a solution containing, for example, 200,000 units of uricase per 1000 ml. is sterilized by filtration and is introduced in a sterile manner into sterile ampoules, at the rate of 5 ml. per ampoule.
- (f) is unaffected by the presence in aqueous solution of any of the anions borate, carbonate, acetate, citrate, nitrate, chloride and phosphate at concen' trations of 10* M to 10- M, the chloride and nitrate ions becoming partial inhibitors of activity at concentrations of 10" M,
- (h) contains the following acids in the following proportions by weight Amino-acids Amino-acids and is obtained by cultivating Aspergillus flavus oryzae No. 624 (ATCC No. 20,047).
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Abstract
Description
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR100673A FR6301M (en) | 1967-03-29 | 1967-03-29 | |
FR100672A FR1529675A (en) | 1967-03-29 | 1967-03-29 | High activity urate oxidase and its preparation |
Publications (1)
Publication Number | Publication Date |
---|---|
US3810820A true US3810820A (en) | 1974-05-14 |
Family
ID=26175159
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US715623A Expired - Lifetime US3620923A (en) | 1967-03-29 | 1968-03-25 | Urate oxidase and process for the production thereof |
US00180220A Expired - Lifetime US3810820A (en) | 1967-03-29 | 1971-09-13 | Urate oxidase and process for the production thereof |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US715623A Expired - Lifetime US3620923A (en) | 1967-03-29 | 1968-03-25 | Urate oxidase and process for the production thereof |
Country Status (12)
Country | Link |
---|---|
US (2) | US3620923A (en) |
JP (1) | JPS5313704B1 (en) |
BE (1) | BE712846A (en) |
CS (1) | CS153458B2 (en) |
DE (1) | DE1642656A1 (en) |
DK (1) | DK127333B (en) |
ES (1) | ES352030A1 (en) |
FR (2) | FR1529675A (en) |
GB (1) | GB1198764A (en) |
NL (1) | NL6804365A (en) |
SE (1) | SE348476B (en) |
SU (1) | SU421162A3 (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4062731A (en) * | 1976-07-21 | 1977-12-13 | Eastman Kodak Company | Production of uricase from micrococcus luteus |
US4064010A (en) * | 1976-07-21 | 1977-12-20 | Eastman Kodak Company | Purification of uricase |
US4273874A (en) * | 1978-12-14 | 1981-06-16 | Kyowa Hakko Kogyo Co., Ltd. | Acidic uricase and process for production thereof |
US4389485A (en) * | 1980-09-19 | 1983-06-21 | E.N.I. Ente Nazionale Idrocarburi | Uricase production method |
US4394450A (en) * | 1982-03-01 | 1983-07-19 | Miles Laboratories, Inc. | Method for purification of uricase |
US4882280A (en) * | 1985-06-05 | 1989-11-21 | Sapporo Breweries Limited | Uricase and a method for the preparation thereof |
FR2649720A1 (en) * | 1989-07-13 | 1991-01-18 | Sanofi Sa | Recombinant gene which encodes a protein such as urate oxidase |
EP0435776A1 (en) * | 1989-12-29 | 1991-07-03 | Sanofi | Artificial promoter for protein expression in yeast |
US5382518A (en) * | 1989-07-13 | 1995-01-17 | Sanofi | Urate oxidase activity protein, recombinant gene coding therefor, expression vector, micro-organisms and transformed cells |
US5407822A (en) * | 1991-10-02 | 1995-04-18 | Sanofi | Artificial promoter for the expression of proteins in yeast |
US9441210B2 (en) | 2013-06-26 | 2016-09-13 | Food Industry Research And Development Institute | Method of reducing levels of uric acid |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2164018C3 (en) * | 1970-12-26 | 1973-11-15 | Noda Institute For Scientific Research, Noda (Japan) | Process for the biotechnological production of Uncase |
NZ234453A (en) * | 1989-07-13 | 1993-01-27 | Sanofi Sa | Recombinant dna encoding urate oxidase, and vector, host, protein and pharmaceutical compositions associated therewith |
FR2656530B1 (en) * | 1989-12-29 | 1994-09-23 | Sanofi Sa | RECOMBINANT GENE FOR EXPRESSION IN EUKARYOTIC CELLS OF A PROTEIN SUCH AS URATE OXIDASE. |
FR2664286B1 (en) * | 1990-07-05 | 1994-09-02 | Sanofi Sa | NOVEL STRAIN OF ASPGILLUS FLAVUS AND ITS USE FOR THE PRODUCTION OF URATE-OXIDASE. |
US5792751A (en) * | 1992-04-13 | 1998-08-11 | Baylor College Of Medicine | Tranformation of cells associated with fluid spaces |
WO1994001139A1 (en) * | 1992-07-13 | 1994-01-20 | Baylor College Of Medicine | Targeting somatic gene therapy to joints |
US6541606B2 (en) * | 1997-12-31 | 2003-04-01 | Altus Biologics Inc. | Stabilized protein crystals formulations containing them and methods of making them |
US6783965B1 (en) * | 2000-02-10 | 2004-08-31 | Mountain View Pharmaceuticals, Inc. | Aggregate-free urate oxidase for preparation of non-immunogenic polymer conjugates |
KR100614212B1 (en) * | 1998-08-06 | 2006-08-21 | 마운틴 뷰 파마슈티컬즈 인크. | Fiji-Urate Oxidase Conjugates and Uses thereof |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1104197A (en) * | 1965-07-28 | 1968-02-21 | Ono Pharmaceutical Co | Method of producing uricase from yeast |
US3431176A (en) * | 1966-02-02 | 1969-03-04 | Toyo Boseki | Preparation of uricase |
-
1967
- 1967-03-29 FR FR100672A patent/FR1529675A/en not_active Expired
- 1967-03-29 FR FR100673A patent/FR6301M/fr not_active Expired
-
1968
- 1968-03-19 DE DE19681642656 patent/DE1642656A1/en active Pending
- 1968-03-25 US US715623A patent/US3620923A/en not_active Expired - Lifetime
- 1968-03-27 GB GB14827/68A patent/GB1198764A/en not_active Expired
- 1968-03-27 ES ES352030A patent/ES352030A1/en not_active Expired
- 1968-03-27 BE BE712846D patent/BE712846A/xx unknown
- 1968-03-27 SE SE04062/68A patent/SE348476B/xx unknown
- 1968-03-28 JP JP1978468A patent/JPS5313704B1/ja active Pending
- 1968-03-28 NL NL6804365A patent/NL6804365A/xx unknown
- 1968-03-28 DK DK135168AA patent/DK127333B/en unknown
- 1968-03-29 CS CS241968A patent/CS153458B2/cs unknown
- 1968-03-29 SU SU1228281A patent/SU421162A3/en active
-
1971
- 1971-09-13 US US00180220A patent/US3810820A/en not_active Expired - Lifetime
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4062731A (en) * | 1976-07-21 | 1977-12-13 | Eastman Kodak Company | Production of uricase from micrococcus luteus |
US4064010A (en) * | 1976-07-21 | 1977-12-20 | Eastman Kodak Company | Purification of uricase |
US4273874A (en) * | 1978-12-14 | 1981-06-16 | Kyowa Hakko Kogyo Co., Ltd. | Acidic uricase and process for production thereof |
US4317878A (en) * | 1978-12-14 | 1982-03-02 | Kyowa Hakko Kogyo Co., Ltd. | Test composition containing acidic uricase used for quantitative determination of uric acid in sample |
US4389485A (en) * | 1980-09-19 | 1983-06-21 | E.N.I. Ente Nazionale Idrocarburi | Uricase production method |
US4394450A (en) * | 1982-03-01 | 1983-07-19 | Miles Laboratories, Inc. | Method for purification of uricase |
US4987076A (en) * | 1985-06-05 | 1991-01-22 | Sapporo Breweries Limited | Uricase and a method for the preparation thereof |
US4882280A (en) * | 1985-06-05 | 1989-11-21 | Sapporo Breweries Limited | Uricase and a method for the preparation thereof |
FR2649720A1 (en) * | 1989-07-13 | 1991-01-18 | Sanofi Sa | Recombinant gene which encodes a protein such as urate oxidase |
US5382518A (en) * | 1989-07-13 | 1995-01-17 | Sanofi | Urate oxidase activity protein, recombinant gene coding therefor, expression vector, micro-organisms and transformed cells |
US5541098A (en) * | 1989-07-13 | 1996-07-30 | Sanofi | Urate oxidase activity protein, recombinant gene coding therefor, expression vector, micro-organisms and transformed cells |
EP0435776A1 (en) * | 1989-12-29 | 1991-07-03 | Sanofi | Artificial promoter for protein expression in yeast |
FR2656531A1 (en) * | 1989-12-29 | 1991-07-05 | Sanofi Sa | ARTIFICIAL PROMOTER FOR THE EXPRESSION OF PROTEINS IN YEAST. |
WO1991009956A1 (en) * | 1989-12-29 | 1991-07-11 | Sanofi | Artificial promoter for expressing proteins in yeast |
US5407822A (en) * | 1991-10-02 | 1995-04-18 | Sanofi | Artificial promoter for the expression of proteins in yeast |
US9441210B2 (en) | 2013-06-26 | 2016-09-13 | Food Industry Research And Development Institute | Method of reducing levels of uric acid |
Also Published As
Publication number | Publication date |
---|---|
ES352030A1 (en) | 1969-07-01 |
GB1198764A (en) | 1970-07-15 |
US3620923A (en) | 1971-11-16 |
FR1529675A (en) | 1968-06-21 |
SU421162A3 (en) | 1974-03-25 |
NL6804365A (en) | 1968-09-30 |
JPS5313704B1 (en) | 1978-05-12 |
FR6301M (en) | 1968-09-09 |
CS153458B2 (en) | 1974-02-25 |
DE1642656A1 (en) | 1971-05-19 |
BE712846A (en) | 1968-07-31 |
SE348476B (en) | 1972-09-04 |
DK127333B (en) | 1973-10-22 |
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Owner name: CM INDUSTRIES Free format text: CHANGE OF NAME;ASSIGNORS:ETABLISSEMENTS CLIN BYLA (CHANGED TO);CLIN MIDY (CHANGED TO);REEL/FRAME:004163/0742 Effective date: 19820311 Owner name: SANOFI Free format text: MERGER;ASSIGNOR:CM INDUSTRIES;REEL/FRAME:004163/0737 Effective date: 19801203 Owner name: SEMPA-CHIMIE, 20 RUE DES FOSSES-SAINT-JACQUES, PAR Free format text: MERGER;ASSIGNOR:SOCIETE D ETUDES ET D APPLICATIONS BIOCHIMIQUES S.E.A.B.,;REEL/FRAME:004163/0754 Effective date: 19740629 Owner name: SANOFI 40, AVENUE GEORGE V, 75008 PARIS A SOCIETE Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:PRODUITS CHIMIQUES UGINE KUHLMANN A SOCETE ANONYME;SEMPA-CHIMIE, A SOCIETE ANONYME;REEL/FRAME:004163/0747 Effective date: 19821018 |